JP4229567B2 - Secondary battery - Google Patents
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- JP4229567B2 JP4229567B2 JP2000089272A JP2000089272A JP4229567B2 JP 4229567 B2 JP4229567 B2 JP 4229567B2 JP 2000089272 A JP2000089272 A JP 2000089272A JP 2000089272 A JP2000089272 A JP 2000089272A JP 4229567 B2 JP4229567 B2 JP 4229567B2
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- H—ELECTRICITY
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- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/134—Electrodes based on metals, Si or alloys
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- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- H01M4/387—Tin or alloys based on tin
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/49002—Electrical device making
- Y10T29/49108—Electric battery cell making
- Y10T29/49115—Electric battery cell making including coating or impregnating
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Description
【０００１】
【発明の属する技術分野】
本発明は、二次電池に関するものであり、詳細には活物質としてＬｉと合金化する活物質粒子を用いた二次電池に関するものである。
【０００２】
【従来の技術】
リチウム金属を負極として用いたリチウム二次電池は、そのエネルギー密度が大きいことから、次世代の二次電池として注目されている。しかしながら、リチウム金属を負極に用いるため、充放電に伴ってリチウム金属の溶解析出が生じ、デンドライトの生成や電極の変形が生じる。このため、サイクル性能が劣悪であり、実用化に耐え得るものはできていない。このような問題を解決し得るものとして、Ｌｉと合金化する金属を用いたＬｉ合金負極や、黒鉛などの炭素材料を用いた炭素負極が提案されており、炭素負極を用いたものは一部実用化されている。
【０００３】
【発明が解決しようとする課題】
しかしながら、炭素負極はその理論容量が３７２ｍＡｈ／ｇと低いため、金属リチウムを負極に用いた場合に比べて、大幅にエネルギー密度が低下するという欠点がある。また、Ｌｉ合金負極を用いた場合には、充放電に伴い体積の膨張と収縮が繰り返されるため、充放電サイクルが進むにつれて活物質粒子が微粉化し、サイクル性能が悪くなるという欠点があった。
【０００４】
本発明の目的は、Ｌｉと合金化する活物質粒子を含む電極を用いた二次電池において、活物質粒子の微粉化を抑制することができ、サイクル性能を飛躍的に向上させることができる二次電池を提供することにある。
【０００５】
【課題を解決するための手段】
本発明の二次電池は、Ｌｉと合金化する活物質粒子を含む電極を用いたリチウム二次電池であり、活物質粒子中にＬｉと合金化しない金属元素が拡散分布していることを特徴としており、Ｌｉと合金化する活物質がＳｉであり、Ｌｉと合金化しない金属元素がＣｕであることを特徴としている。
【０００６】
本発明に従う第１の局面においては、Ｌｉと合金化しない金属元素の濃度が、活物質粒子の内部から表面に向かうにつれて増加していることを特徴としており、Ｓｉ粉末の表面上にＣｕ層を形成した後、熱処理してＳｉ粉末中にＣｕを拡散させ、Ｓｉ粉末内部から表面に向うにつれてＣｕ濃度が増加する濃度分布が付与された活物質粒子を負極活物質として用いたことを特徴としている。
本発明に従う第１の局面の製造方法は、Ｓｉ粉末の表面上にＣｕ層を形成した後、熱処理してＳｉ粉末中にＣｕを拡散させ、Ｓｉ粉末内部から表面に向うにつれてＣｕ濃度が増加する濃度分布をＳｉ粉末に付与することを特徴としている。
【０００７】
本発明に従う第２の局面においては、Ｌｉと合金化しない金属元素の濃度が、活物質粒子の内部から表面に向かうにつれて減少していることを特徴としており、Ｃｕ粉末の表面上にＳｉ層を形成した後、熱処理してＣｕ粉末中にＳｉを拡散させ、Ｃｕ粉末内部から表面に向うにつれてＣｕ濃度が減少する濃度分布が付与された活物質粒子を負極活物質として用いたことを特徴としている。
本発明に従う第２の局面の製造方法は、Ｃｕ粉末の表面上にＳｉ層を形成した後、熱処理してＣｕ粉末中にＳｉを拡散させ、Ｃｕ粉末内部から表面に向うにつれてＣｕ濃度が減少する濃度分布をＣｕ粉末に付与することを特徴としている。
【００１１】
（作用効果）
一般に電極活物質は粉末状の活物質を結着剤で結着して作製される。従って、電極反応の場となるのは活物質としての粉末自体である。粉末状の活物質にＬｉが吸蔵される場合、先ず粉末表面からＬｉが入っていく。一般に、Ｌｉが活物質に入り合金化されると、その体積が膨張するため、粉末の表面は膨張するが、内部はＬｉが入っていないため膨張しない。従って、表面と内部での膨張率が大きく異なり、粉末が割れて微粉化する。この表面と内部の膨張率の差を調整することにより、微粉化を抑制することができる。本発明においては、Ｌｉと合金化しない金属元素を、活物質粒子中に拡散分布することにより、このような表面と内部の膨張率の差を小さくして、微粉化を抑制している。
【００１２】
本発明の第１の局面では、Ｌｉと合金化しない金属元素が、活物質粒子の内部から表面に向かうにつれて増加する濃度分布を有している。このような場合、表面ではＬｉと合金化しない金属元素の濃度が高く、活物質の濃度が低くなっているため、Ｌｉを吸蔵しても表面の膨張率が小さく、Ｌｉが吸蔵されていない内部との膨張率の差がそれ程大きいものとはならない。従って、内部応力が小さくなり、活物質粒子の割れを抑制することができる。
【００１３】
本発明の第２の局面では、上記金属元素が、活物質粒子の内部から表面に向かうにつれて減少する濃度分布を有している。このような場合、粒子表面の活物質濃度は高いので、表面の膨張は大きく、内部の膨張は小さくなり、内部応力が大きくなる。しかしながら、粒子内部では活物質濃度が低いため、粒子表面で発生した割れは、粒子内部までは到達せず、粒子表面のみが割れた状態となる。この結果、粒子全体としては微粉化せず、微粉化が抑制された状態となる。
【００１４】
本発明の第１の局面に従い、Ｌｉと合金化しない金属元素の濃度が活物質粒子の内部から表面に向かうにつれて増加している活物質粒子を作製する方法としては、種々の方法が考えられるが、例えば以下の方法が挙げられる。
【００１５】
▲１▼Ｌｉと合金化する活物質粒子の表面上に無電解鍍金により、Ｌｉと合金化しない金属元素の層を設けた後、適当な温度で熱処理し、金属元素を活物質粒子の表面から内部に拡散させる方法。
【００１６】
Ｌｉと合金化する活物質粒子としてＳｉ粉末を用い、金属元素としてＣｕを用いる場合、Ｓｉ粉末の表面上に、無電解鍍金によりＣｕ層を形成した後、熱処理してＳｉ粉末中にＣｕを拡散させ、Ｓｉ粉末内部から表面に向かうにつれてＣｕの濃度が連続的に増加するような濃度分布を付与することができる。
【００１７】
▲２▼Ｌｉと合金化する活物質粒子の表面上に、Ｌｉと合金化しない金属元素の層をメカノフージョン法により形成した後、適当な温度で熱処理し、金属元素を活物質粒子の表面から内部に拡散させる方法。
【００１８】
Ｌｉと合金化する活物質粒子としてＳｉ粒子を用い、金属元素としてＣｕを用いる場合、Ｓｉ粉末とＣｕ微粒子とを機械的に混合しメカノフージョン法によりＳｉ粉末の表面にＣｕ層を形成し、その後適当な温度で熱処理してＳｉ粉末中にＣｕを拡散させ、Ｓｉ粉末内部から表面に向かうにつれてＣｕの濃度が連続的に増加する濃度分布を付与することができる。
【００１９】
本発明の第２の局面に従い、Ｌｉと合金化しない金属元素の濃度が、Ｌｉと合金化する活物質粒子の内部から表面に向かうにつれ減少している活物質粒子を製造する方法としては、種々の方法が考えられるが、例えば以下の方法が挙げられる。
【００２０】
▲３▼Ｌｉと合金化しない金属粒子の表面上に、無電解鍍金によりＬｉと合金化する活物質の層を設けた後、適当な温度で熱処理する方法。
例えば、Ｌｉと合金化する活物質としてＧｅを用い、Ｌｉと合金化しない金属元素としてＣｕを用いる場合、このような方法で作製できる。
【００２１】
▲４▼Ｌｉと合金化しない金属粒子の表面上に、メカノフージョン法によりＬｉと合金化する活物質の層を形成した後、適当な温度で熱処理する方法。
Ｌｉと合金化する活物質としてＳｉを用い、Ｌｉと合金化しない金属元素としてＣｕを用いる場合、Ｃｕ粉末とＳｉ微粒子とを機械的に混合しメカノフージョン法により、Ｃｕ粉末上にＳｉ層を形成した後、適当な温度で熱処理して、ＳｉをＣｕ粉末中に拡散させ、粒子内部から表面に向かうにつれてＣｕが減少している濃度分布を付与することができる。
【００２２】
▲５▼Ｌｉと合金化しない金属粒子の表面上に、活物質の酸化物の層をメカノフージョン法等により形成した後、水素気流などの還元雰囲気中で該酸化物を適当な温度で還元すると同時に、この還元された活物質を金属粒子中に拡散させる方法。
【００２３】
Ｌｉと合金化する活物質としてＳｉを用い、Ｌｉと合金化しない金属元素としてＣｕを用いる場合、Ｃｕ粉末の上にＳｉＯ層またはＳｉＯ2 層をメカノフージョン法またはその他の方法により形成し、水素気流等の還元性雰囲気中でこの酸化物を適当な温度で還元させると同時に、還元により形成されたＳｉをＣｕ粒子中に拡散させ、粒子の内部から表面に向かうにつれてＣｕの濃度が減少している濃度分布を付与することができる。
【００２４】
上記▲１▼〜▲５▼の場合において、金属元素を拡散させるための熱処理の温度は、絶対温度基準で、拡散する金属の融点の約１／１０〜４／５程度室温から上昇させた温度の範囲内であることが好ましい。
【００２５】
【発明の実施の形態】
以下、本発明を実施例に基づいてさらに詳細に説明するが、本発明は以下の実施例に何ら限定されるものではなく、その要旨を変更しない範囲において適宜変更して実施することが可能なものである。
【００２６】
〔本発明電池の作製〕
（負極活物質の作製）
平均粒径１μｍのＳｉ粉末１００ｇを、表１に示す組成の３５℃の水溶液５００ｃｃに３分間浸漬した後、水洗し、１０体積％のＨＣｌ水溶液に５分間浸漬することにより、Ｓｉ粉末の表面に無電解鍍金の触媒となるＰｄ核を形成した。
【００２７】
【表１】
次に、このＳｉ粉末を、表面がＣｕ色になるまで、表２に示す組成のｐＨ１２．５に調整した無電解鍍金浴に浸漬した。このようにして表面にＣｕ層を形成したＳｉ粉末を、５００℃真空下で熱処理して、Ｓｉ粉末中にＣｕを拡散させた。
【００２９】
【表２】
上記の熱処理により、Ｓｉ粉末中にＣｕが拡散していることを確認するため、Ｓｉ粉末の代わりに、Ｃｕ箔の上に膜厚２μｍのＳｉ膜をＣＶＤ法により形成し、これを熱処理してＳｉ薄膜中にＣｕが拡散していることをＳＩＭＳ分析により確認した。図１は、この結果を示す図である。図１に示すように、Ｓｉ薄膜中にＣｕが存在しており、Ｓｉ薄膜中にＣｕが拡散していることがわかる。また、Ｓｉ薄膜中のＣｕは、Ｓｉ薄膜の内部から表面に向かうにつれて増加していることがわかる。従って、上記のＳｉ粉末の場合においても、Ｓｉ粉末中にＣｕが拡散しており、内部から表面に向かうにつれてＣｕの濃度が増加する濃度分布を有していることがわかる。
【００３１】
（作用極の作製）
上記で作製した負極活物質１００ｇを、結着剤であるフッ素樹脂（ＰＶｄＦ）が５％となるように溶解されたＮ−メチルピロリドン溶液に混合し、３０分らいかい機でらいかいしてスラリーを作製した。このスラリーをドクターブレード法によって厚み１８μｍの電解銅箔上に塗布し、乾燥して、２×２ｃｍの大きさに切り出し、作用極とした。
【００３２】
（対極の作製）
厚み０．９ｍｍのＬｉ金属を３×３ｃｍの大きさに切り出し、対極とした。
（試験セルの作製）
上記で作製した作用極と対極を、ポリプロピレン製セパレータを介して重ねた後、ガラス板を挟んで、電解液中に浸漬し、試験セルを作製した。これらの電極群と接しないようにＬｉ金属を電解液に浸漬し、参照極とした。なお、電解液としては、エチレンカーボネートとジエチルカーボネートの等体積混合溶媒に、ＬｉＰＦ6 を１モル／リットル溶解したものを用いた。
【００３３】
〔比較電池の作製〕
平均粒径１μｍのＳｉ粉末１００ｇをそのまま負極活物質として用いる以外は、上記試験セルと同様にして比較試験セルを作製し、比較電池Ａとした。また、平均粒径１μｍのケイ化銅粉末１００ｇをそのまま負極活物質として用いる以外は、上記試験セルと同様にして比較試験セルを作製し、比較電池Ｂとした。
【００３４】
〔充放電サイクル試験〕
充電はＬｉ基準で０Ｖまでとし、放電はＬｉ基準で２Ｖまでとし、充放電電流は０．５ｍＡとして、上記各試験セルの充放電サイクル試験を行った。表３に、各試験セルの放電容量と充放電効率を示す。
【００３５】
【表３】
表３に示すように、本発明電池は、比較電池Ａ及びＢに比べ、サイクル数を重ねても、高い放電容量を示しており、また良好な充放電効率を示している。１０サイクル後の試験セルを分解したところ、本発明電池においては、試験セルの負極活物質は若干、集電体であるＣｕ箔から剥離している部分があったものの、負極活物質自体は形状を保っていた。これに対し、比較電池Ａ及びＢにおいては、負極活物質がほとんど集電体から剥離し、負極活物質自体も形状を保っておらず、微粉化が進行し、大部分は電解液中に分散し脱落しているのが確認された。
【００３７】
以上のように、本発明電池は、充放電サイクル試験によっても微粉化が生じず、優れたサイクル特性を示すものである。
【００３８】
【発明の効果】
本発明によれば、活物質粒子の微粉化を抑制することができ、サイクル性能を飛躍的に向上させることができる。
【図面の簡単な説明】
【図１】Ｃｕ箔の上に形成したＳｉ膜を熱処理した後の、ＳＩＭＳ分析によるＣｕ濃度分布を示す図。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a secondary battery, and more particularly, to a secondary battery using active material particles alloyed with Li as an active material.
[0002]
[Prior art]
A lithium secondary battery using lithium metal as a negative electrode has attracted attention as a next-generation secondary battery because of its high energy density. However, since lithium metal is used for the negative electrode, lithium metal dissolves and precipitates with charge and discharge, and dendrites are generated and the electrode is deformed. For this reason, cycle performance is inferior, and what can endure practical use has not been made. As a solution to such a problem, a Li alloy negative electrode using a metal alloying with Li and a carbon negative electrode using a carbon material such as graphite have been proposed. It has been put into practical use.
[0003]
[Problems to be solved by the invention]
However, since the theoretical capacity of the carbon negative electrode is as low as 372 mAh / g, there is a drawback that the energy density is greatly reduced as compared with the case where metallic lithium is used for the negative electrode. Further, when a Li alloy negative electrode is used, volume expansion and contraction are repeated with charge / discharge, so that the active material particles are pulverized as the charge / discharge cycle progresses, resulting in poor cycle performance.
[0004]
An object of the present invention is to reduce the pulverization of active material particles in a secondary battery using an electrode including active material particles alloyed with Li, and to dramatically improve cycle performance. The next battery is to provide.
[0005]
[Means for Solving the Problems]
The secondary battery of the present invention is a lithium secondary battery using an electrode including active material particles that are alloyed with Li, wherein a metal element that does not alloy with Li is diffusely distributed in the active material particles. The active material that is alloyed with Li is Si, and the metal element that is not alloyed with Li is Cu.
[0006]
In the first aspect according to the present invention, the concentration of the metal element that does not alloy with Li increases from the inside of the active material particles toward the surface, and a Cu layer is formed on the surface of the Si powder. After the formation, heat treatment is performed to diffuse Cu in the Si powder, and active material particles having a concentration distribution in which the Cu concentration increases from the inside of the Si powder toward the surface are used as the negative electrode active material . .
In the manufacturing method of the first aspect according to the present invention, after forming a Cu layer on the surface of the Si powder, heat treatment is performed to diffuse Cu in the Si powder, and the Cu concentration increases from the inside of the Si powder toward the surface. It is characterized by imparting a concentration distribution to the Si powder.
[0007]
In the second aspect according to the present invention, the concentration of the metal element that does not alloy with Li decreases from the inside of the active material particles toward the surface, and a Si layer is formed on the surface of the Cu powder. After the formation, heat treatment is performed to diffuse Si in the Cu powder, and active material particles having a concentration distribution in which the Cu concentration decreases from the inside of the Cu powder toward the surface are used as the negative electrode active material . .
In the manufacturing method of the second aspect according to the present invention, after forming the Si layer on the surface of the Cu powder, heat treatment is performed to diffuse Si into the Cu powder, and the Cu concentration decreases from the inside of the Cu powder toward the surface. It is characterized by imparting a concentration distribution to the Cu powder.
[0011]
(Function and effect)
In general, an electrode active material is produced by binding a powdered active material with a binder. Therefore, the electrode reaction field is the powder itself as the active material. When Li is occluded in the powdered active material, Li first enters from the powder surface. Generally, when Li enters an active material and is alloyed, its volume expands, so the surface of the powder expands, but the interior does not expand because it does not contain Li. Therefore, the expansion coefficients on the surface and inside are greatly different, and the powder is cracked and pulverized. By adjusting the difference in expansion coefficient between the surface and the inside, pulverization can be suppressed. In the present invention, the metal element that is not alloyed with Li is diffused and distributed in the active material particles, thereby reducing the difference in the expansion coefficient between the surface and the inside, thereby suppressing pulverization.
[0012]
In the first aspect of the present invention, the metal element that does not alloy with Li has a concentration distribution that increases from the inside to the surface of the active material particles. In such a case, the concentration of the metal element that is not alloyed with Li is high on the surface, and the concentration of the active material is low. Therefore, even if Li is occluded, the surface expansion coefficient is small, and Li is not occluded. The difference in the expansion rate with is not so large. Accordingly, the internal stress is reduced and cracking of the active material particles can be suppressed.
[0013]
In the second aspect of the present invention, the metal element has a concentration distribution that decreases from the inside to the surface of the active material particles. In such a case, since the active material concentration on the particle surface is high, the surface expansion is large, the internal expansion is small, and the internal stress is large. However, since the active material concentration is low inside the particle, the crack generated on the particle surface does not reach the inside of the particle, and only the particle surface is broken. As a result, the particles as a whole are not pulverized and the pulverization is suppressed.
[0014]
According to the first aspect of the present invention, various methods can be considered as a method for producing active material particles in which the concentration of a metal element that is not alloyed with Li increases from the inside to the surface of the active material particles. For example, the following methods can be mentioned.
[0015]
(1) A layer of a metal element that is not alloyed with Li is formed on the surface of the active material particles to be alloyed with Li by electroless plating, and then heat-treated at an appropriate temperature to remove the metal element from the surface of the active material particles. How to diffuse inside.
[0016]
When Si powder is used as the active material particles to be alloyed with Li and Cu is used as the metal element, a Cu layer is formed on the surface of the Si powder by electroless plating and then heat-treated to diffuse Cu into the Si powder. Thus, a concentration distribution in which the concentration of Cu continuously increases from the inside of the Si powder toward the surface can be provided.
[0017]
(2) A metal element layer that is not alloyed with Li is formed on the surface of the active material particles that are alloyed with Li by a mechano-fusion method, and then heat-treated at an appropriate temperature to remove the metal elements from the surface of the active material particles. How to diffuse inside.
[0018]
When Si particles are used as active material particles to be alloyed with Li and Cu is used as a metal element, Si powder and Cu fine particles are mechanically mixed to form a Cu layer on the surface of the Si powder by a mechano-fusion method, and thereafter Heat treatment can be performed at an appropriate temperature to diffuse Cu into the Si powder, and a concentration distribution in which the concentration of Cu continuously increases from the inside to the surface of the Si powder can be imparted.
[0019]
According to the second aspect of the present invention, there are various methods for producing active material particles in which the concentration of a metal element that is not alloyed with Li decreases from the inside of the active material particles that are alloyed with Li toward the surface. For example, the following methods can be mentioned.
[0020]
(3) A method in which a layer of an active material that is alloyed with Li is formed by electroless plating on the surface of metal particles that are not alloyed with Li, and then heat-treated at an appropriate temperature.
For example, when Ge is used as an active material to be alloyed with Li and Cu is used as a metal element that is not alloyed with Li, it can be produced by such a method.
[0021]
(4) A method in which a layer of an active material that is alloyed with Li is formed on the surface of metal particles that are not alloyed with Li by a mechano-fusion method and then heat-treated at an appropriate temperature.
When Si is used as an active material to be alloyed with Li and Cu is used as a metal element that is not alloyed with Li, Cu powder and Si fine particles are mechanically mixed to form a Si layer on the Cu powder by a mechanofusion method. After that, heat treatment can be performed at an appropriate temperature to diffuse Si into the Cu powder, thereby giving a concentration distribution in which Cu decreases from the inside of the particle toward the surface.
[0022]
(5) After forming an oxide layer of an active material on the surface of metal particles not alloyed with Li by a mechano-fusion method or the like, the oxide is reduced at an appropriate temperature in a reducing atmosphere such as a hydrogen stream. At the same time, the reduced active material is diffused into the metal particles.
[0023]
When Si is used as an active material to be alloyed with Li and Cu is used as a metal element that is not alloyed with Li, a SiO layer or SiO 2 layer is formed on the Cu powder by a mechano-fusion method or other methods, and a hydrogen gas flow This oxide is reduced at an appropriate temperature in a reducing atmosphere such as Si, and simultaneously, Si formed by the reduction is diffused in the Cu particles, and the concentration of Cu decreases from the inside of the particles toward the surface. A concentration distribution can be imparted.
[0024]
In the case of (1) to (5) above, the temperature of the heat treatment for diffusing the metal element is a temperature raised from room temperature by about 1/10 to 4/5 of the melting point of the diffusing metal on an absolute temperature basis. It is preferable to be within the range.
[0025]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in more detail based on examples. However, the present invention is not limited to the following examples, and can be implemented with appropriate modifications within a range not changing the gist thereof. Is.
[0026]
[Preparation of the battery of the present invention]
(Preparation of negative electrode active material)
After immersing 100 g of Si powder having an average particle size of 1 μm in 500 cc of 35 ° C. aqueous solution having the composition shown in Table 1 for 3 minutes, washing with water and immersing in 10% by volume of HCl aqueous solution for 5 minutes, Pd nuclei serving as a catalyst for electroless plating were formed.
[0027]
[Table 1]
Next, this Si powder was immersed in an electroless plating bath adjusted to pH 12.5 having the composition shown in Table 2 until the surface became Cu color. The Si powder having the Cu layer formed on the surface in this manner was heat-treated at 500 ° C. under vacuum to diffuse Cu into the Si powder.
[0029]
[Table 2]
In order to confirm that Cu has diffused in the Si powder by the above heat treatment, instead of the Si powder, a 2 μm-thick Si film is formed on the Cu foil by the CVD method, and this is heat-treated. It was confirmed by SIMS analysis that Cu was diffused in the Si thin film. FIG. 1 is a diagram showing the results. As shown in FIG. 1, it can be seen that Cu is present in the Si thin film and Cu is diffused in the Si thin film. Moreover, it turns out that Cu in Si thin film is increasing as it goes to the surface from the inside of Si thin film. Therefore, it can be seen that even in the case of the Si powder, Cu diffuses in the Si powder and has a concentration distribution in which the concentration of Cu increases from the inside toward the surface.
[0031]
(Production of working electrode)
100 g of the negative electrode active material prepared above is mixed with an N-methylpyrrolidone solution in which a fluororesin (PVdF) serving as a binder is 5%, and the slurry is stirred for 30 minutes. Was made. This slurry was applied onto an electrolytic copper foil having a thickness of 18 μm by a doctor blade method, dried, cut into a size of 2 × 2 cm, and used as a working electrode.
[0032]
(Production of counter electrode)
Li metal with a thickness of 0.9 mm was cut into a size of 3 × 3 cm and used as a counter electrode.
(Production of test cell)
The working electrode and counter electrode produced above were stacked via a polypropylene separator, and then immersed in an electrolytic solution with a glass plate sandwiched therebetween to produce a test cell. Li metal was immersed in an electrolytic solution so as not to contact these electrode groups, and used as a reference electrode. As the electrolytic solution, an equal volume mixed solvent of ethylene carbonate and diethyl carbonate was used as the LiPF 6 was dissolved 1 mol / liter.
[0033]
[Production of comparative battery]
A comparative test cell was prepared as Comparative battery A in the same manner as the test cell except that 100 g of Si powder having an average particle diameter of 1 μm was used as it was as the negative electrode active material. In addition, a comparative test cell was prepared in the same manner as the above test cell except that 100 g of copper silicide powder having an average particle diameter of 1 μm was used as it was as the negative electrode active material.
[0034]
[Charge / discharge cycle test]
The charge and discharge cycle tests of each of the above test cells were performed with charging up to 0 V on the basis of Li, discharging up to 2 V on the basis of Li, and charging and discharging current of 0.5 mA. Table 3 shows the discharge capacity and charge / discharge efficiency of each test cell.
[0035]
[Table 3]
As shown in Table 3, the battery of the present invention shows a high discharge capacity and good charge / discharge efficiency even when the number of cycles is repeated as compared with the comparative batteries A and B. When the test cell after 10 cycles was disassembled, in the battery of the present invention, the negative electrode active material of the test cell was slightly peeled off from the Cu foil as the current collector, but the negative electrode active material itself was shaped. Was kept. On the other hand, in comparative batteries A and B, the negative electrode active material almost peeled off from the current collector, the negative electrode active material itself did not maintain its shape, and pulverization progressed, and the majority was dispersed in the electrolyte. It was confirmed that it was missing.
[0037]
As described above, the battery of the present invention does not cause pulverization even in the charge / discharge cycle test, and exhibits excellent cycle characteristics.
[0038]
【The invention's effect】
According to the present invention, pulverization of active material particles can be suppressed, and cycle performance can be dramatically improved.
[Brief description of the drawings]
FIG. 1 is a view showing a Cu concentration distribution by SIMS analysis after heat-treating a Si film formed on a Cu foil.
Claims (4)
Priority Applications (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000089272A JP4229567B2 (en) | 2000-03-28 | 2000-03-28 | Secondary battery |
| KR10-2002-7012777A KR100483408B1 (en) | 2000-03-28 | 2001-03-15 | Method of Manufacturing an Electrode Active Material Particle for a Rechargeable Battery |
| PCT/JP2001/002048 WO2001073872A1 (en) | 2000-03-28 | 2001-03-15 | Rechargeable battery |
| DE60142778T DE60142778D1 (en) | 2000-03-28 | 2001-03-15 | Process for producing a particle from an electrode-active material |
| EP01912387A EP1271674B1 (en) | 2000-03-28 | 2001-03-15 | Method of manufacturing an electrode active material particle |
| US10/239,745 US7316717B2 (en) | 2000-03-28 | 2001-03-15 | Method of manufacturing an electrode active material particle for a rechargeable battery |
| AU2001241149A AU2001241149A1 (en) | 2000-03-28 | 2001-03-15 | Rechargeable battery |
| CNB018071775A CN1241278C (en) | 2000-03-28 | 2001-03-15 | Rechargeable battery |
| HK03105538A HK1053390A1 (en) | 2000-03-28 | 2003-08-01 | Method for preparing rechargeable battery electrode containing particles of an active material |
| US11/979,915 US7655273B2 (en) | 2000-03-28 | 2007-11-09 | Method of manufacturing an electrode active material particle for a rechargeable battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000089272A JP4229567B2 (en) | 2000-03-28 | 2000-03-28 | Secondary battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001273892A JP2001273892A (en) | 2001-10-05 |
| JP4229567B2 true JP4229567B2 (en) | 2009-02-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000089272A Expired - Fee Related JP4229567B2 (en) | 2000-03-28 | 2000-03-28 | Secondary battery |
Country Status (9)
| Country | Link |
|---|---|
| US (2) | US7316717B2 (en) |
| EP (1) | EP1271674B1 (en) |
| JP (1) | JP4229567B2 (en) |
| KR (1) | KR100483408B1 (en) |
| CN (1) | CN1241278C (en) |
| AU (1) | AU2001241149A1 (en) |
| DE (1) | DE60142778D1 (en) |
| HK (1) | HK1053390A1 (en) |
| WO (1) | WO2001073872A1 (en) |
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| CN1280930C (en) * | 2000-09-01 | 2006-10-18 | 三洋电机株式会社 | Negative electrode for lithium secondary cell and method for producing the same |
| EP1313158A3 (en) * | 2001-11-20 | 2004-09-08 | Canon Kabushiki Kaisha | Electrode material for rechargeable lithium battery, electrode comprising said electrode material, rechargeable lithium battery having said electrode , and process for the production thereof |
| EP2302720B1 (en) * | 2003-03-26 | 2012-06-27 | Canon Kabushiki Kaisha | Electrode material for lithium secondary battery and electrode structure including the same |
| JP4061586B2 (en) * | 2003-04-11 | 2008-03-19 | ソニー株式会社 | Positive electrode active material for nonaqueous electrolyte secondary battery and nonaqueous electrolyte secondary battery using the same |
| AU2003289402A1 (en) * | 2003-04-23 | 2004-11-19 | Mitsui Mining And Smelting Co., Ltd. | Negative electrode for nonaqueous electrolyte secondary battery, method for manufacturing same and nonaqueous electrolyte secondary battery |
| US20050118502A1 (en) * | 2003-11-27 | 2005-06-02 | Matsushita Electric Industrial Co., Ltd. | Energy device and method for producing the same |
| US20060121345A1 (en) * | 2003-12-04 | 2006-06-08 | Kiyotaka Yasuda | Electrode for secondary battery, process of producing the electrode, and secondary battery |
| JP2005197080A (en) * | 2004-01-07 | 2005-07-21 | Nec Corp | Anode for secondary battery and secondary battery using it |
| JP2005293852A (en) * | 2004-03-31 | 2005-10-20 | Sanyo Electric Co Ltd | Manufacturing method of lithium secondary battery and anode for the lithium secondary battery |
| JP4953610B2 (en) | 2005-09-29 | 2012-06-13 | 三洋電機株式会社 | Lithium secondary battery |
| US20100062340A1 (en) * | 2005-11-08 | 2010-03-11 | Mitsui Mining & Smelting Co., Ltd. | Negative electrode for nonaqueous secondary battery |
| JP2007213825A (en) * | 2006-02-07 | 2007-08-23 | Matsushita Electric Ind Co Ltd | Nonaqueous electrolyte secondary battery, anode activator and anode of the same, as well as manufacturing method of nonaqueous electrolyte secondary battery, anode activator, and anode of the same |
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| JP5245425B2 (en) * | 2007-06-05 | 2013-07-24 | ソニー株式会社 | Negative electrode and secondary battery |
| JP2009176719A (en) * | 2007-12-26 | 2009-08-06 | Sony Corp | Electrolyte, secondary battery, and sulfone compound |
| JP5520538B2 (en) * | 2009-08-03 | 2014-06-11 | 古河電気工業株式会社 | Negative electrode material for lithium ion secondary battery containing nano-sized particles, negative electrode for lithium ion secondary battery, lithium ion secondary battery |
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| JP5581716B2 (en) | 2010-02-05 | 2014-09-03 | ソニー株式会社 | Negative electrode for lithium ion secondary battery, lithium ion secondary battery, electric tool, electric vehicle and power storage system |
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| JP2011165402A (en) | 2010-02-05 | 2011-08-25 | Sony Corp | Anode for lithium ion secondary battery, lithium ion secondary battery, power tool, electric vehicle, and power storage system |
| JP5187335B2 (en) * | 2010-03-29 | 2013-04-24 | 日本電気株式会社 | Negative electrode for secondary battery and method for producing the same, secondary battery |
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| JP6156190B2 (en) * | 2014-02-27 | 2017-07-05 | ソニー株式会社 | Negative electrode active material, battery, battery pack, electronic device, electric vehicle, power storage device, and power system |
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-
2000
- 2000-03-28 JP JP2000089272A patent/JP4229567B2/en not_active Expired - Fee Related
-
2001
- 2001-03-15 EP EP01912387A patent/EP1271674B1/en not_active Expired - Lifetime
- 2001-03-15 KR KR10-2002-7012777A patent/KR100483408B1/en not_active IP Right Cessation
- 2001-03-15 CN CNB018071775A patent/CN1241278C/en not_active Expired - Fee Related
- 2001-03-15 DE DE60142778T patent/DE60142778D1/en not_active Expired - Lifetime
- 2001-03-15 US US10/239,745 patent/US7316717B2/en not_active Expired - Lifetime
- 2001-03-15 WO PCT/JP2001/002048 patent/WO2001073872A1/en active IP Right Grant
- 2001-03-15 AU AU2001241149A patent/AU2001241149A1/en not_active Abandoned
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2003
- 2003-08-01 HK HK03105538A patent/HK1053390A1/en not_active IP Right Cessation
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2007
- 2007-11-09 US US11/979,915 patent/US7655273B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EP1271674B1 (en) | 2010-08-11 |
| HK1053390A1 (en) | 2003-10-17 |
| KR20020086710A (en) | 2002-11-18 |
| US20080226816A1 (en) | 2008-09-18 |
| JP2001273892A (en) | 2001-10-05 |
| AU2001241149A1 (en) | 2001-10-08 |
| KR100483408B1 (en) | 2005-04-15 |
| EP1271674A4 (en) | 2007-09-05 |
| US7655273B2 (en) | 2010-02-02 |
| WO2001073872A1 (en) | 2001-10-04 |
| EP1271674A1 (en) | 2003-01-02 |
| US7316717B2 (en) | 2008-01-08 |
| DE60142778D1 (en) | 2010-09-23 |
| US20040058245A1 (en) | 2004-03-25 |
| CN1419716A (en) | 2003-05-21 |
| CN1241278C (en) | 2006-02-08 |
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